Fermentation method

• US 4,460,687 A
• Filed: 09/14/1983
• Issued: 07/17/1984
• Est. Priority Date: 03/23/1981
• Status: Expired due to Fees

• Current Assignee: ALFA Laval AB
• Original Assignee: ALFA Laval AB
• Inventors: Ehnstrom, Lars K. J.
• Primary Examiner(s): Penland, R. B.
• Application Number:
  US06/532,042
• Time in Patent Office: 307 Days
• Field of Search: 435/161, 435/162, 435/165, 435/256, 435/813, 426/31, 426/53, 426/429, 426/431, 426/493, 426/494
• US Class Current: 435/161
• CPC Class Codes: C12P 7/06 Ethanol, i.e. non-beverage
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y10S 435/813 Continuous fermentation

Abstract

A continuous process for producing ethanol by fermenting carbohydrate containing feed stocks at atmospheric pressure in a fermentor, in which a fermentation liquor stream is withdrawn from the fermentor, a yeast concentrate is recovered from said stream both recycled to the fermentor and the yeast-free remainder treated to remove ethanol and leave a stillage stream, a large portion of which is recycled to the fermentor, enabling high concentration of fermentable material to be supplied to the fermentor and reducing the amount of water required for the process.

Claims

1. In the production of ethanol by the continuous fermentation of a carbohydrate containing substrate at about atmospheric pressure in a continuous process circuit comprising a fermentor in which an amount of active yeast cells sufficient to achieve an ethanol productivity in the range of 5-20 kg/h ethanol per cubic meter of fermentor liquid volume is maintained by continuous yeast recirculation, the improvement which consists essentially of continuously charging into said process circuit a feed stream containing at least 18% by weight of yeast-fermentable carbohydrates, having a concentration and flow rate sufficient to supply yeast fermentable carbohydrates in accordance with said ethanol productivity to maintain a steady state concentration of fermentable substance in the fermentor at less than 2% by weight, continuously withdrawing a stream of fermentation liquor from the fermentor at a flow rate sufficeint to maintain a steady state ethanol concentration in the fermentor in the range of 3-7% weight, continuously separating said stream of fermentation liquor, in a centrifugal separation step, into at least one continuous yeast concentrate stream and an essentially yeast-free stream, continuously returning said yeast concentrate stream to the fermentor, continuously separating said yeast-free stream into an ethanol-enriched stream, and a residual stream, continuously discharging said ethanol enriched stream from the circuit, continuously discharging part of said residual stream from the circuit in an amount sufficient to balance the amount of non fermentable substances charged to the circuit, heating the remaining part of said residual stream to at least about 60°

C. and continuously recirculating said heated part of said residual stream to the fermentor.

2. The method of claim 1, further consisting essentially of distilling the yeast-free stream to effect its separation.

3. The method of claim 1, further consisting essentially of screening said stream of fermentation to form a reject fraction and a screened fraction, conveying said screened fraction to said centrifugal separation step, and returning said reject fraction to the circuit downstream of said centrifugal separation step.

4. The method of claim 1, further consisting essentially of mechanically separating said residual stream into a first fraction enriched in solid substance, and a second fraction with reduced solid content, discharging said first fraction from the circuit and returning at least part of said second fraction to the fermentor.

5. The method of claim 4, further consisting essentially of further separating said first fraction enriched in solid substance in a mechanical thickening step, into a third fraction further enriched in solid substance, and a fourth fraction poor in solids, discharging said third fraction from the circuit and returning to the fermentor at least a part of said fourth fraction.

6. The method of claim 5 further consisting essentially of thickening said first fraction in a decanter.

7. The method of claim 1, further consisting essentially of saccharifying the feed stream in a saccharifying step and returning at least part of said remaining part of said residual stream to said saccharifying step.

8. The method of claim 2, further consisting essentially of charging direct steam to said distillation step as a heating medium.

9. The metod of claim 1, further consisting essentially of maintaining a concentration of fermentable substance in the fermentor less than 0.5% by weight.

10. The method of claim 9 further consisting essentially of maintaining said concentration at less than 0.2% by weight.